A method is provided for removing sulphur-containing gases from fossil fuel-fired combustors comprising the step of introducing sorbent particles modified with lignosulfonates into the exhaust gases.
|
3. A lignosulfonate-modified calcium hydroxide containing up to 5% by weight calcium lignosulfonate, having a finer particle size distribution than a corresponding non-surfactant modified sorbent.
1. A method for preparing particulate calcium hydroxide/calcium lignosulfonate sorbent comprising the steps of contacting calcium oxide with water at a water to calcium oxide ratio of 2.6 with said water containing a sufficient amount of calcium lignosulfonate to result in the crystallization of calcium hydroxide/calcium lignosulfonate particles containing up to 5% by weight calcium lignosulfonate.
5. A method for reducing agglomeration and enhancing the handling characteristics of dry particulate calcium hydroxide or dry particulate calcium magnesium hydroxide comprising the step of hydrating calcium oxide or a mixture of calcium oxide and magnesium oxide in the presence of a sufficient amount of alkali metal lignosulfonate to produce up to 5% by weight of said lignosulfonate in said dry particulate hydroxide and said lignosulfonate.
2. A method according to
4. A lignosulfonate-modified calcium hydroxide according to
|
|||||||||||||||||||||||||||||
This is a division of application Ser. No. 930,689, filed Nov. 12, 1986,now U.S. Pat. No. 4,786,485.
The present invention is directed to a method for removing sulphur-containing gases from the exhaust gases of a fossil fuel-fired combustor. In particular, the present method provides for removing sulphur-containing gases by introducing particulate surfactant-modified sorbent downstream of the flame zone of the combustor.
Relatively costly methods exist for control of sulphur oxide pollution from fossil fuel-fired combustors, but they are most commonly applied to new facilities where the expense and control of the technology is justifiable due to the long remaining depreciable lifetime of the facility. There is a large population of older combustors in existence for which the cost-effective methods of reducing sulphur oxide emissions are not generally available due to the substantial additional capital expense which would need to be expended on an old facility. There is a need, therefore, to develop cost-efficient, retrofittable technology to control sulphur oxides and nitrogen oxides in this population of older plants.
In other methods, inorganic promoters have been added to each of the calcium-based sorbents in an effort to increase their reactivity. Promoters can increase reactivity significantly but each group of effective promoters has problems which preclude it from practical application. Transition metals such as chromium are effective in various forms but they are relatively expensive and may produce environmental side effects of their own. Alkali metal additives are aggressive promoters during natural gas-firing, but are condensed on the ash which is produced during coal-firing and are unavailable to promote SO2 capture by the sorbent. There remains a need in the art, therefore, for a sorbent with an improved capability of capturing SO2 that will not be depleted by ash interactions in a coal-fired combustor, and which does not introduce detrimental environmental effects.
It is thus an object of the present invention to provide a method for removing sulpher-containing gases, particularly sulphur oxides, from the exhausts of fossil fuel-fired combustors.
It is also an object of the present invention to provide an improved sorbent for removing sulphur oxides from the exhaust gases of fossil fuel-fired combustors when said sorbent is injected into, or downstream from the combustor.
These and other objects of the present invention will be apparent from the following description and appended claims.
In accompanying drawings:
FIG. 1 is a graph of the amount of increase in calcium utilization (over unmodified control sorbent) in the sorbent utilized in accordance with the present invention versus the amount of lignosulfonate concentration in the sorbent.
FIG. 2 is a graph showing the comparison in the amounts of calcium utilization versus the calcium/sulphur ratio in two sorbents, with and without the improvement according to the present invention.
The present invention provides a method for removing sulphur-containing gases from exhaust gases of fossil fuel-fired combustors comprising the step of introducing into the exhaust gases sorbent particles capable of reacting with sulphur oxides wherein the particles comprise calcium hydroxide or calcium magnesium hydroxide and an ionic surfactant. The surfactant is preferably an alkali metal lignosulfonate. The sorbent preferably comprises 1 to 2 percent by weight calcium lignosulfonate but may contain up to 5 percent by weight calcium lignosulfonate, and is characterized by a significantly finer particle size distribution than the equivalent sorbent without lignosulfonate.
To practice the method according to the present invention, a surfactant-modified sorbent is prepared. The preferred surfactant is an alkali metal lignosulfonate. The sorbent is selected from the group consisting of calcium magnesium hydroxide [Ca(OH)2.Mg(OH)2 ] and calcium hydroxide [Ca(OH)2 ]. Initially, limestone (CaCO3) or dolomite [CaMg(CO3)2 ] is calcined to its respective oxide (CaO or CaO.MgO), usually in the temperature range of 900° to 1100°C (lime temperature) but preferably at around 1000° C. This produces a soft-burned lime characteristic of that available at commercial lime plants. The resulting oxide is then hydrated at a water to oxide ratio ranging from 2 to 3 but preferably around 2.6, with water containing the desired amount of calcium lignosulfonate or other ionic surfactant. The amount of calcium lignosulfonate utilized will be that sufficient to produce a resulting calcium hydroxide/calcium lignosulfonate product containing up to about 5 percent by weight calcium lignosulfonate. Preferably, the resulting product will contain about 1 to 2 percent calcium lignosulfonate.
The calcium lignosulfonate-modified calcium hydroxide sorbent according to the present invention results in a higher capture of SO2 than an unmodified calcium hydroxide when injected into a fossil fuel-fired combustor or combustor flue system. Typically the modified sorbent will be injected into the flue where the exhaust gases are at a temperature in the range of about 65° to 1230°C Since the improved performance is the result of a physical rather than a chemical change, the tendency of coal ash to remove the enhancement is avoided.
The lignosulfonate-modified sorbents are also improved in that they have improved handling characteristics. Commercial hydrates frequently have the tendencies to cake and agglomerate during storage and handling which cause problems at their point of use. The lignosulfonate-modified sorbents according to the present invention are characterized by a reduced amount of caking during storage and reduced amount of agglomeration during handling, thus facilitating handling and controllability of fluidization during feeding to the reactor or combustor.
While not intending to be bound to any particular theory of operation of the present invention, it is believed that the surfactant-modified sorbents according to the present invention exhibit these improved properties, at least in part, because of formation of smaller calcium hydroxide particles. Smaller particles are formed in two ways: (1) during the hydration reaction, surfactant decreases the surface energy of the nucleus/solution interface (surface tension) and thereby increases the nucleation rate. This results in a large number of small crystals rather than a small number of large crystals; (2) the tendency of small calcium hydroxide crystals to form larger particles through agglomeration is reduced by eliminating the layer of adsorbed water which surrounds such crystals. This is accomplished by introducing a hydrophobic surfactant layer around the crystals. Thus, both an increase in nucleation rate during the hydration reaction, and a decrease in adsorbed water by enhanced by hydrophobicity of crystal surfaces are effected by a small quantity of lignosulfonate.
Having described the preferred embodiment of the present invention the following examples are provided for purposes of illustration. However, the examples are not intended to limit the invention in any way.
A commercially available limestone, Presque Isle, was calcined to calcium oxide at 1000°C for 16 hours. A chemical analysis of the resulting lime showed no significant quantities of known inorganic promoters. The resulting calcium oxide was then hydrated at a water to calcium oxide ratio of 2.6 with water containing varying amounts of calcium lignosulfonate. The amounts of the calcium lignosulfonate surfactant in the water were calculated to yield 0, 0.5, 1.0, 1.5, 2.0, 3.0, 4.0, and 5.0% of calcium lignosulfonate in the product calcium hydroxide. The modified calcium hydroxides were then tested for reactivity with sulphur dioxide in a laboratory scale isothermal flow reactor in which the reactor temperature was held at 1000°C, the residence time for the reaction was 1 second, and the sulphur dioxide concentration was 3000 ppm. These are conditions within the range of those which would be encountered during downstream injection of a sorbent for SO2 capture in a coal-fired boiler. The increased calcium utilization by the sorbent-containing calcium lignosulfonate over the control sorbent (containing no surfactant) are shown in FIG. 1. At the optimum calcium lignosulfonate concentrations in the hydroxide (1.5 to 2.0 weight percent), calcium utilization increases of approximately 5% absolute (20 to 25% relative) is achieved. With calcium to sulphur ratio of 2 an SO2 capture of over 60% is calculated.
Two sorbents were produced for testing in a pilot-scale, coal-fired combustor. The control sorbent was commercial Longview calcium hydroxide. The modified sorbent was made from commerical Longview calcium oxdie, experimentally hydrated with water containing calcium lignosulfonate to produce a hydroxide containing 1% calcium lignosulfonate. The sorbent was then injected into a 106 Btu, coal-fired furnace at 1250°C The resulting calcium utilizations of the control and modified sorbents are shown in FIG. 2. A 20 to 25% relative increase in calcium utilization by the modified sorbent is shown.
Kirchgessner, David A., Lorrain, Jeffrey M.
| Patent | Priority | Assignee | Title |
| 11365150, | Jul 18 2018 | Mississippi Lime Company | Lime hydrate with improved reactivity via additives |
| 5427994, | Nov 12 1986 | The United States of America as represented by the Environmental | Lignosulfonate-modified calcium hydroxide for SO2 control during furnace injection |
| 7354485, | May 27 2005 | EARTH ALIVE CLEAN TECHNOLOGIES INC | Cleaning solution |
| Patent | Priority | Assignee | Title |
| JP5393190, |
| Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
| Aug 09 1988 | United States of America Environmental Protection Agency | (assignment on the face of the patent) | / | |||
| Dec 18 1998 | BELLEFONTE LIME COMPANY | MONTREAL TRUST COMPANY OF CANADA | SECURITY AGREEMENT | 009731 | /0677 |
| Date | Maintenance Fee Events |
| Jan 19 1993 | ASPN: Payor Number Assigned. |
| May 05 1993 | M183: Payment of Maintenance Fee, 4th Year, Large Entity. |
| May 21 1997 | M184: Payment of Maintenance Fee, 8th Year, Large Entity. |
| May 21 2001 | M185: Payment of Maintenance Fee, 12th Year, Large Entity. |
| Date | Maintenance Schedule |
| Nov 21 1992 | 4 years fee payment window open |
| May 21 1993 | 6 months grace period start (w surcharge) |
| Nov 21 1993 | patent expiry (for year 4) |
| Nov 21 1995 | 2 years to revive unintentionally abandoned end. (for year 4) |
| Nov 21 1996 | 8 years fee payment window open |
| May 21 1997 | 6 months grace period start (w surcharge) |
| Nov 21 1997 | patent expiry (for year 8) |
| Nov 21 1999 | 2 years to revive unintentionally abandoned end. (for year 8) |
| Nov 21 2000 | 12 years fee payment window open |
| May 21 2001 | 6 months grace period start (w surcharge) |
| Nov 21 2001 | patent expiry (for year 12) |
| Nov 21 2003 | 2 years to revive unintentionally abandoned end. (for year 12) |